Thermoplastic plastic composition

ABSTRACT

REVERSIBLE CROSS-LINKING IS IMPARTED TO POLYMERS AND COPOLYMERS ESPECIALLY OF THE VINYL, OLEFINIC AND OLEFINIC OXIDE TYPES BY MEANS OF RECURRING DICYCLOPENTADIENE LINKAGES. DIFUNCTIONAL DICYCLOPENTADIENE COMPOUNDS CAN BE POLYMERIZED DIRECTLY INTO HOMOPOLYMERS OR POLYMERIZED WITH COMONOMERS TO FORM COPOLYMERS. ALTERNATIVELY, POLYMERS CARRYING CYCLOPENTADIENE SUBSTITUENTS CAN BE PREPARED AND THE DIMERIZATION OF THE CYCLOPENTADIENE GROUPS EFFECTED IN SITU TO PRODUCE THE CROSS-LINKAGES. THE DICYCLOPENTADIENE CROSS-LINKAGES CLEAVE ON HEATING TO A SUFFICIENT TEMPERATURE SO THAT THE PRESENT POLYMERS AND COPOLYMERS HAVE A THERMOPLASTIC CHARACTER NOTWITHSTANDING THEIR NORMAL CROSS-LINKED NETWORK STRUCTURE.

y 1974 YASUHIRO TAKESHITA ETAL 3,826,760

'IHERIOPLASTIC PLASTIC COMPOSITIQN Filed 090. 22, 1971 r 3 Sheets-Sheet 1 O D 1% U LI 0 F/G. F/G. 2.

160 200 360 C K50 2 00 360 C Patented July 30, 1974 3,826,760 THERMOPLASTIC PLASTIC COMPOSITION Yasuhiro Takeshita, Michitake Uoi, Yoshiyuki Hirai, and Mitsuru Uchiyama, Chiba, Japan, assignors to 'Idemitsu Kosan Co., Ltd., Tokyo, Japan Filed Dec. 22, 1971, Ser. No. 210,834 Claims priority, application Japan, Dec. 26, 1970, 45/128,474, 45/128,475; Sept. 29, 1971, 46/75,427, 46/ 75,428

Int. Cl. C08f 1/86, 3/16; C08g 30/00 us, or. 260--2 EP 7 Claims ABSTRACT or THE DISCLOSURE This invention relates to thermoplastic plastic composition comprising novel cross-linked .polymers or copolyrners, to a process for producing the plastics, to a shaping process using the plastics and to 'the shaped articles. In other-.aspects, this invention relates to a novel linear polymer'or copolymer that is a' precursor of the cross-linked polymers or copolymers and to a process for producing the linear polymer or copolymer.

Plastics have been used widely as one of the most important materials in a variety of fields. It is well known that plastics are classified into thermosetting plastics and thermoplastic plastics and that both kinds of plastics are largely different in their properties.

Thermosetting plastics are converted by heating into insoluble and infusible substances, thus giving products excellent in chemical resistance, heat-resistance and dimensional stability, but are inferior in workabilty and working efficiency. On the other hand, thermoplastic plastics are .easily softened by heating and are soluble in various organicsolvents, thus attaining good workability andhigh working elficiency, but are inferior in heatresistance, chemical resistance and dimensional stability. The, glifference in the properties between both kinds of plastics is-ascribable to the-fact that moldings of thermosetting plastics normally have a complicated network structure, while moldings of thermoplastic plastics have a linear structure. If there are plastics which have a network structure and are easily shaped by heating, they will possessess the merits of both kinds of plastics. Such plastics have earnestly been desired in the plastic industry fora long time.

Various researches have been made with a purpose of development of plastics which have a cross-linking structure and which can'easily be shaped by heating and have now found that polymers or copolymers having a network structure cross-linked through dicyclopentadiene rings are temporarily cleaved to be plasticized at cross-linkages by heating at av certain temperature, but such. cross-linkages are reformed to reinstate the network structure when the heated polymers or copolymers are cooled. Such polymers or copolymers cross-linked through dicyclopentadiene rings are novel substances which have not been described in literatures.

Thus, it is an object of this invention to provide thermoplastic plastics comprising polymers or copolymers cross-linked through dicyclopentadiene rings. It is another object of this invention to provide a process for producing polymers or coplymers having a substantially network structure cross-linked through dicyclopentadiene rings.

It is a further object of this invention to provide a shaped method for manufacturing shaped articles effectively from the thermoplastic plastics.

It is still another object of this invention to provide shaped articles of the thermoplastic plastics.

It is a further object of this invention to provide new linear polymers or copolymers which are precursors of the cross-linked polymers or copolymers.

It is still a further object of this invention to provide a process for producing the linear polymers or copolymers.

These and other objects of this invention will become apparent as the description proceeds.

The aforementioned objects can be attained by practicing this invention as will be stated hereinafter.

The thermoplastic plastics of this invention comprise polymers or copolymers having a substantially network structure cross-linked through dicyclopentadiene rings of the formula:

A preferred example of the thermoplastics of this invention is a polymer or copolymer having a recurring crosslinked structure unit of the general formula:

l l re O CH: or i')-0 radical A and A each represent a substituted or unsubstituted lower alkylene or oxyalkylene group, m and m. are zero or a positive integer of at least 1.

The cross-linked polymers or copolymers are produced by the two different processes as will be described hereinafter.

One process for producing the cross-linked polymers or copolymers comprises dimerizing a cyclopentadiene compound having an olefinically unsaturated group or glycidyl group to form a dicyclopentadiene compound having two olefinically unsaturated groups or glycidyl groups and then copolymerizing the dicyclopentadiene compound alone or in mixture with other copolymerizable olefinically unsaturated compounds or glycidyl compounds. The cyclopentadiene compounds having an olefinically unsaturated group or glycidyl group which are utilizable as starting material in this process include cyclopentadienes substituted by an alkenyl group, such as allylcyclopentadiene or methallylcyclopentadiene; a'i-kenyl esters of a carboxylic acid having cyclopentadiene ring, such as vinyl cyclopentadiene carboxylate or allyl cyclopentadiene carboxylate; cyclopentadicnyl esters of a carboxylic acid having an olefinically unsaturated group, such as cyclopentadienyl acrylate or cyclopentadienyl methacrylate; and glycidyl compounds such as glycidylcyclopentadiene, glycidyl cyclopentadienecarboxylate or cyclopentadienyl glycidate. If desired, the cyclopentadiene ring in these compounds may carry an inert substituent such as an alkyl group.

The cyclopentadiene compounds having an olefinically unsaturated group or glycidyl group are prepared as will be described hereinafter.

For example, cyclopentadienyl compounds substituted by an alkenyl group or glycidyl group can be prepared easily by reacting cyclopentadiene with an alkali metal such as sodium in a suitable solvent, for example, tetrahydrofuran, pentahydropyran, dioxane or a mixture thereof with an aromatic hydrocarbon, to form an alkali metal salt of cyclopentadiene and then reacting the salt directly or indirectly with an alkenylating agent such as an alkenyl halide or a glycidylating agent such as a glycidyl halide. Alkenyl or glycidyl esters of cyclopentadienecarboxylic acid are prepared by the alkali salt of cyclopentadiene with carbon dioxide to form cyclopentadienecarboxylic acid and then subjecting the acid to transesterification reaction with an alkenyl or glycidyl ester of a fatty acid. Other cyclopentadiene compounds can be prepared according to a similar manner.

The cyclopentadiene compounds having an olefinically unsaturated group or glycidyl group thus obtained are readily dimerized by heating at a temperature, for example, up to 140 C. to form dicyclopentadiene compounds having two olefinically unsaturated groups or glycidyl groups. The dicyclopentadiene compounds having two olefinically unsaturated groups or glycidyl groups may be homopolymerized but are preferably copolymerized with other copolymerizable monomers to form crosslinked copolymers. Such copolymerizable monomers include, for example, olefins such as ethylene, propylene and butylene; dienes such as butadiene and isoprene; styrenes such as styrene itself, a-methylstyrene, and mand p-methylstyrene; unsaturated carboxylic acids or esters thereof such as acrylic acid, methacrylic acid, methyl acrylate and ethyl methacrylate; vinyl esters such as vinyl acetate and vinyl propionate; halogenated olefins such as vinyl chloride, vinyl fluoride and vinylidene chloride; and olefine oxides such as ethylene oxide and propylene oxide. Besides these, any of the copolymerizable monomers can be employed unless it affords a thermosetting plastic when homopolymerized. As catalysts for the copolymerization, there can be used adequately cationic catalysts, anionic catalysts, complex catalysts or radical initiators conventionally used for the polymerization reaction of this type.

During this polymerization reaction, the dicyclopentadiene rings may be cleaved to give polymers or copolymers soluble in solvents.

Another process for producing the cross-linked polymers or copolymers comprises reacting an alkali metal salt of cyclopentadiene with a halogenomethylated polyether obtained by polymerization or copolymerization of an epihalohydrin to form a linear polymer having pendant cyclopentadiene rings and then heating the linear polymer at temperatures up to 150 C. to effect cross-linking.

The polymers or copolymers of an epihalohydrin used as starting material are prepared in a conventional manner by subjecting an epihalohydrin either alone or in mixture with one or more of the comonomers selected from the group consisting of an alkylene oxide and a cyclic ether to bulk polymerization reaction or solution polymerization reaction conducted at a reaction temperature of from room temperature to 50 C. for at least minutes in the pres ence of a catalyst system consisting of an alkyl metal such as diethylzinc or alkylaluminum and water. The alkylene oxide as the comonomer includes ethylene oxide, propylene oxide, styrene oxide, etc., and the cyclic ether includes tetrahydrofuran, oxetane, etc. The linear polymers or c0- polymers having pendant cyclopentadienyl groups are obtained by dissolving the polymer or copolymer of an epihalohydrin obtained as above in a suitable organic solvent, e.g., tetrahydrofuran or a mixture of tctrahydrofuran and an aromatic hydrocarbon such as benzene, toluene or the like, and adding dropwise to the solution an alkali metal compound of cyclopentadiene at a temperature not exceeding 30 C. In this case, the concentration of the polymer or copolymer in the solvent is selected within the range of at most 5% by weight, preferably within the range of 1.0-3.0% by weight.

A polyether having a recurring unit of the formula:

Wherein n is zero or a positive integer of at least 1, is thus obtained.

This polyether is a new self-curable polymer which, just after production, is in the form of liquid or unvulcanized rubber but permits a mutual reaction between the pendant cyclopentadiene rings in vicinal molecules to form a cross-linking structure, thus resulting in a rubbery elastomer.

Polymers or copolymers of this invention are excellent in chemical resistance and dimensional stability and are insoluble in organic solvents, similar to conventional thermosetting plastics but, when heated at a predetermined temperature above C., for example, higher than 210 C. as to styrene copolymers, higher than 150 C. as to butadiene copolymers, and higher than C. as to ethylene copolymers, the cross-linking structure is degraded to make the compounds fluid and, consequently, the compounds in this state can readily be molded by any desired means such as injection molding, extrusion molding and cast molding. The plastics molded as described above are gradually cooled to form the cross-linking structure again whereby they are no longer soluble in organic solvents sich as benzene, toluene and Decalin.

Through the molding temperature to be adopted in the shaping process of this invention depends on the kind of the main molecular chain, it is usually within the range of -150- 400 C. and preferably 200300 C.

The moldings thus produced are excellent products which are free from defects of conventional thermoplastic plastics but have almost all of the merits of thermosetting plastics.

Below is an example of a preferred embodiment of the shaping process of this invention. About 10 grams of a powdery cross-linked polymer obtained by copolymerization of methallylcyclopentad'iene dimer and butadiene in an equimolar proportion were molded with an injection molder under the conditions of 700 kg./cm. injection pressure, 200 C. cylinder temperature and 80 C. metal die temperature.

The molding thus produced was very rigid, had properties comparable with those of thermosetting plastics, and was insoluble in a variety of organic solvents.

The fact that cross-linkages in the cross-linked copolymer of this invention cleave at a certain temperature or high temperatures is understood from the phenomenon that the copolymer becomes soluble in organic solvents such as benzene or toluene and also from a thermogram obtained with a differential thermal analyzer.

FIG. '1 is a thermogram obtained by using a methallylcyclopentadiene dimer/butadiene (2:1) copolymer and FIG. 2 is a thermogram of polybutadiene.

In FIG. 1, the heat absorption peak at 58 C. is coincident with the primary transition point of a solid, and that at 119 C. is coincident with the crystal melting point of transpolybutadiene. A moderate heat absorption peak at temperatures from 132 C. to 287 C., is not found in the thermogram of polybutadiene shown in FIG. 2 and is understood to be based on the thermal cleavage of dicyclopentadiene rings. According to the thermograms, the lower limit of the heating temperature to be used in the shaping process of this invention can be easily found. Though the heating temperature in this invention depends onthe polymers or copolymers to be employed, it is readily selected by obtaining the terminal point of the heat absorption peak due to cleavage of dicyclopentadiene ringsshown'in the thermo'gram and simultaneously taking the decomposition point of the polymer into consideration.

'As thepolyrn'ers or copolymers of this invention crosslinked through dicyclopentadiene rings possess such as pecu'lia'r property that they become thermoplastic above a certain temperature in spite of their three-dimensional network structure, they can be utilized as thermoplastic plastics in' various 'fields of industry. The linear polymers or copolymers having pendant cyclopentadiene rings produced"a s' precursor "of the thermoplastic plastics can widely 'be utilized, as self-curable plastics in the fields of rubber industry and the rfra'chineryl industry for manu facturing various machi tiery'parts;

Thisinvention will be lliistrated more in detail by way of examples. which ar'e' riot intended to limit the scope of'tlfisinvention. j

"EXAMPLE 1 .(A) Synthesis of Allylcyclopentadiene Dimer In 1' l'iterfour-nec ked flask provided with a gas inlet, a condenser "and 'anagitator were placed about 200 ml. of Xyleheand 4 6 g. 2 gram-atom) of metallic sodium. The charge was heated'under agitation to pulverize sodinmfAfter cooling, the xylene was removed and 500 mlfof te'trahydrofuran were added; Then, 180 ml. (about 2 trials) of cy'clopentadiene were added dropwise to the mixture through a dropping funnel at temperatures lower tha n 30 C. whereby generation of hydrogen gas was observed. After the add-ition of cyclopentadiene, the mixture was continuously agitatedtor'a' while, and then .187 mol at allyl bromide were added dropwise thereto with the reaction temperature being kept at 10-20 C. After completion of the addition, the reaction product was filtered to remove the formed sodium chloride and then subjected'to distillation under reduced pressure to obtain 74 g. of allylcyclopentadiene. The yield was 30%.

Allylcycflopentadiene thus obtained were heated at 100 C; -for one hour, wherebymore than 80% of each compoiind was dimerized.

I .1013) Preparation of Cross-linked Copolymer Into a pressure-resistant gas reactor, 185 ml. of toluene, 4 millimols of ethyl-aluminium dichloride and l millimol o fyanadium oxytrichloride were charged and the mixturejyla'siigitated at 20 to.produce a catalyst.

Ta le catalyst wasaddedlO ml. (9.60 g.) of the methallylcyclgpehtadiepe. dimer which was produced in the above"(A)"and 12120 g. of butadiene and the mixture was polymerized at,;2 0 C. for 2.5.hours. The reaction was .stop'pcdby the addition of methanol containing a small amount of hydrochloric acid. The copolymer was taken up in alarge amount of methanol and filtered. The, copolyme'r was dried; under pressure to obtain 10.0 gfof white powdery copolymer. The copolymer thus produced. was recognized tohave cross-linkages as itwas insolublein hot toluene. (It was not completely crosslinked, as-- CH radicalswere observed in infrared ab.- sorption spectr um.) The copolymer was subjected to the test using a flow tester with 170 kg. load and a nozzle having a diameter of 1 mm. whereby the copolymer-began to flow at150 C.

The copolymer was analyzed with a differential thermal analyzer (DSC) to obtain a thermogram shown in FIG. 1 wherein the heat absorption peak at 50 C. is the primary transition point of a solid and the peak at 119 C. is themelting point of the crystal of transpolybutadiene.

[See, G. Natta et al.: Chim. Ind. (Milano) Vol. 47, p. 716 (1965).] The heat absorption peak from 132 C. to 287 C. was not seen in the thermogram of homopolymer of butadiene shown in :FIG. '2 and was recognized to be the heat absorption peak due to thermal cleavage of dicyclopentadiene. The heat absorption peak was confirmed not to result from decomposition of the copolymer by a thermobalance.

The copolymer was heated up to 280 C., cooled to room temperature, and again heated. The thermogram in this case is shown in FIG. 3. The heat absorption peak due to thermal cleavage of dicyclopentadiene was observed at the same temperature as in FIG. 1. This means that cross-linkage, once cleaved, was formed again. According to these facts, it was found that a cross-linked copolymer was formed, fluidized on heating as in the case of thermoplastic copolymers and then cross-linked again.

EXAMPLE 2 Into the same reactor used in Example 1 were charged 180 ml. of toluene, 4 mg. of ethyl aluminum dichloride and 1 millimol of vanadium oxytriohloride to prepare a catalyst. 14.4 grams of the allylcyclopentadiene dimer produced in a manner similar to that described in Example 1i(A) and 18.6 grams of butadiene were added and subjected to polymerization at 20 C. for 2. 5 hours. The product was similarly treated as in Example 1 to obtain 8.2 grams of a copolymer. The copolymer was insoluble was described in Example 1 but fluid on heating and gave the thermogram similar to that in Example 1.

EXAMPLE 3 In 300 ml. two-necked flask were placed 200 ml. of heptane and 3.84 g. of the allylcyclopentadiene dimer produced in a manner similar to that described in Example 1(A). The polymerization took place immediately after adding 2 millimol of diethyl aluminium chloride and 1 millimol of vanadium oxytrichloride as catalyst while blowing ethylene into the mixture at 20 C., resulting in the formation of a copolymer in a suspended state. The polymerization was carried out for 1.5 hours at 20 C. and the polymer produced was precipitated by the addi tion of methanol containing a small amount of hydrochloric acid. The precipitate was filtered and dried to obtain 12.2 g. of a white copolymer. The product was not a cross-linked copolymer as it was soluble in Decalin at C. However, it became insoluble by heating at C. for 15 minutes, and began to flow at C. by a flow tester with 300 kg. load and a nozzle having a diameter of 1 mm. In the thermogram of the heat-treated copolymer, a heat absorption peak was observed at 150 C., besides the melting point of polyethylene, which coincided with the heat absorption peak of the copolymer shown in Example 2.

EXAMPLE 4 (A) Synthesis of Vinyl Cyclopentadienecarboxylate Dimer Metallic sodium was reacted with cyclopentadiene as described in Example 1(A) and the reaction product was poured over Dry Ice whereby the reaction immediately took place to form sodium salt of cyclopentadienecarboxylic acid. The yield was about 100%.

The sodium cyclopentadienecarboxylate thus obtained was hydrolyzed with acid to obtain cyclopentadienecarboxylic acid. v

110 grams (1 mol) of dry ,cyclopentadienecarboxylic acid and 860 g. (10 mols) of vinyl acetatae were allowed to react under reflux for 2 hours in the presence of a c atalyst consisting of mercury acetate and sulfuric acid. After the end of the reaction, unreacted vinyl acetate and formed acetic acid were removed from the extract to obtain vinyl esters of cyclopentadienecarboxylic acid with a rough yield of 90%. The product was heated at,130l50 C. to produce vinyl cyclopentadienecarboxylate dimer.

Into a 30 ml. ampoule were charged 10 ml. of styrene and vinyl cyclopentadienecarboxylate dimer obtained in Referential Example. The ampoule was closed under reduced pressure and put in a thermostat kept at 150 C. whereby almost all of the dimer was converted into vinyl cyclopentadienecarboxylate. After polymerizing at 150 C. for 2 hours, the produced copolymer was taken out. The copolymer was soluble in benzene at room temperature and precipitated by the addition of methanol. After filtering, the precipitated was dried under reduced pressure to obtain 7.63 g. of a copolymer. According to the DSC thermogram of the copolymenit was not recognized to be homopolystyrene. A heat absorption peak was seen at temperatures of 200-270 C. The peak appeared as cyclopentadiene was dimerized on heating and began to cleave at 200 C.

EXAMPLE 5 (A) Synthesis of Methallylcyclopentadiene Dimer In an analogous manner to that described in Eaxmple 1(A) except that 192 ml. of methallyl chloride was used in place of 187 ml. of allyl bromide in Example 1(A), Example 1(A) was repeated to obtain 144 g. of methallylcyclopentadiene in a yield of 60%.

Methallylcyclopentadiene thus obtained was heated at 100 C. for 1 hour to obtain its dimer in a yield of 80% or higher.

(B) Preparation of Cross-linked Copolymer Into 200 cc. two-necked flask were charged 94 ml. of toluene and 4.80 g. of methallylcyclopentadiene dimer obtained in the above (A). To this mixture was then added 91.5 grams of isobutylene with the temperature being kept at 78 C. 0.5 millimol of ethyl aluminum dichloride and 0.25 millimol of vanadium oxytrichloride were added to initiate polymerization. After contininug the polymerization at 78 C. for 5 hours, the product was precipitated by the addition of methanol and dried to obtain 65.0 g. of a copolymer which was a cross-linked copolymer insoluble in benzene.

polymerized in the presence of a catalyst consisting of 4 mililmols of ethyl aluminum dichloride and 1 millimol'of vanadium oxytrichloride at 20 C. for 2.5 hours to obtain 10.0 g. of a copolymer which was insoluble in hot toluene. The copolymer was subjected to a fiow test under the same conditions as described in Example 1 whereby it began to flow at 150 C. and entirely flowed at 220 C. The flowing copolymer was collected and cooled whereby it became again insoluble in hot toluene.

EXAMPLE 8 To 90 ml. of n-heptane were added as catalyst 2 millimols of diethyl aluminum chloride and 1 millimol of vanadium oxytrichloride, 9.8 g. of -allylcyclopentadiene dimer obtained in a manner similar to that described in Example 1(A) were then addedto the mixture and ethylene was blown thereinto. The polymerization was carried out at 25 C. for 1 hour. to produce 7.8 g. of. a copolymer which was soluble in Decalin while hot (130 C.). When the copolymer was heated at 150 EXAMPLE 9 v (A) Preparation of a Polymer of Epichlorohydrin Into a three-necked flask which had been purged of air by argon were charged in turn epichlorohydrin which had been dehydrated and purified by calcium hydride, n-heptane, water and diethylzinc to conduct polym-' eriza'tion of epichlorohydrin.

After the lapse of a predeterminedreaction time, thepolymerization mixture was poured into a large excess of a methanol/aqueous hydrochloric acid mixture to -precipitate an epichlorohydrin polymer which was then sufficiently washed and dried under reduced pressure.

The polymerization conditions and results were asindicated in the following Table 1.

TABLE 1 r v Dlethyl- Yield at Eplehlorohydrln n-Heptane Water zinc Temperature Time polymer (ml.) (mmol) (mmol) 0.) (hr.)

2 2 Room bemp.;.... 12 0. 0 40 5 5 d0 12 19.0 40 10 10 do 12 11.0

EXAMPLE 6 50.5 milliliters of styrene, 3.65 g. of cyclopentadiene carboxylate dimer produced in a manner similar to that described in Example 4(A), 100 ml. of water, 1.5 g. of sodium laurate and 0.25 g. of potassium persulfate were subjected to emulsion polymerization reaction at 3040 C. for 5.5 hours to obtian 39.6 g. of a copolymer. In elementary analysis, the copolymer was found to obtain 5.6% vinyl cyclopentadienecarboxylate unit. The copolymer was understood to have cross-linkages, as it was insoluble in hot benzene.

The copolymer was subjected to a fluid test using a Koka-type flow tester. The copolymer began to flow at 210 C. under the conditions of 170 kg. load, 1 mm. of the nozzle diameter and 6 C./min. of the temperature elevating rate, and entirely flowed at 295 C. The flowing copolymer was taken out and cooled whereby it again became insoluble in hot benzene.

EXAMPLE 7 ..tractor to prepare a polymer solution of a polymer concentration of 3.0% by weight. A predetermined amount of the polymer solution' was chargedinto a flask which had been purged of air by argon a 0.005 mol percent solution of cyclopentadienylsodium in tetrahydrofuran was then added dropwise thereto and the mixture was maintained at temperatures of 0 to 5 C. for 3 hours to effect reaction. The reaction mixture was then concentrated and poured into a' large excess of water to obtain a precipitate which was sufiiciently washed with water and then with methanoland dried under reduced pressure.

The results of the elementary analysis on the reaction product thus obtained are summarized in the following Table 2. The results summarized in Table 2 indicate that the chlorine content of the starting polymer decreased 1 with the reaction and that there occurred reaction between chlorine atoms in the polymer and cyclopentadienyl sodium.

TABLE 2 Cyclopentadiene ring con- Amount of charged Elementary analysis tent (mol C.P.-Na (mol percent, (percent by weight) percent of based on C1 in the reaction polymer) 1 C H 01 product) 1 l Cyclopentadienylsodium.

1 Calculated based on the C and Cl contents of reaction product determined by elementary analysis.

1 Starting polymer (epichlorohydn'n polymer).

The resultant reaction product was confirmed to be a propylene oxide-epichlorohydrin copolymer having cyclopentadiene rings by the results of an elementary analysis and an infrared absorption spectrum analysis.

The copolymer was then heated at 140 C. for 1 hour to eifect cross-linking reaction. As a result, there was obltained a solvent-insoluble elastomer in the form of a ge EXAMPLE 11 (A) Preparation of Epichlorohydrin/Tetrahydro1 furan/Ethylene Oxide Terpolymer TABLE 4 Tetra- Elementary analysis Epichlorohydro- Trlethyl- Yield of Melee (percent by weight) Ethylene oxide hydrln iuran aluminum Water eopolym r ular (mmol) (mmol) (mmol) (mmol) (mmol) (g.) weight C H C magnumi380 emf- 1530 cut- 1560 Gin-' and 1630-cm." which-are absent in that of FIG. 4.

' "(C) Preparation of Cross-linked Copolymer Thereaction products having cyclopentadiene ring contents of 1.8, 3.0 and 4.2 molpercent, respectively, were heated at 140 C. for l h'o'ur to 'eifect cross-linking reaction. As the results, there were obtained elastomers which were insoluble in solvents lhe infrared absorption spectral diagram -o1i"-the elastomers-= is shown in FIG. 6 where the absorption peaks at 680 cmr 810 cm.- and l380'--cm-.- shown inF1655 are' disappeared and the peakat 900-om." -becomes little-By these facts, it was confirmed that a dicyclopentadiene cross-linked structure was formed-in the elastomer.

y i Q J XAMET-EJQ.

(A) Preparation of atCopolymer of Epichlorohydrin and Propylene Oxide.

Into a three-necked flask which had been purged of air .by: argonwere charged in turn propylene oxide, epichlorohydrin, toluene, waterand =triethylaluminum and the charge was maintained at room-temperature for 50 hours to.,couduct polymerization. Thefreaction mixture was .then poured into a-water/methanol/dilute hydrochloric acid mixture to. precipitate a polymerizate which was dried overnightunder reduced pressure to obtain a propylene oxide epichlorohydrincopolymer.

The polymerization conditions and results were as in dicated-in the following Table 3.

(B) Preparation of Cross-linked Terpolymer In 50 ml. of tetrahydrofuran was dissolved 1.2 g. of the resulting terpolymer having a chlorine content of 2.7% by weight. To the polymer solution were added dropwise ml. of a tetrahydrofuran solution containing 10 m-mol of cyclopen-tadienylsodium at temperatures of 0 to 10 C. and, thereafter, the mixture was maintained at room temperature for 3 hours to conduct reaction.

After completion of the reaction, the reaction mixture was concentrated and poured into water to obtain a precipitate which was washed with water and dried under reduced pressure. The polymer thus obtained had a reduced chlorine content of 1.6% by weight. The polymer converted into a rubbery polymer when heated at 140 C. under pressure of 5 kg./cm. for 1 hour.

(A) Preparation of Epichlorohydrin/Tetrahydrofuran Copolymer precipitated in methanol, added to a dilute aqueous hy- LE TAB a Chlorine content Propylene Eplchlorw v 'lriethyl Yield of Molecoteooxlde hydrin -Toluene aluminum Water copolymer ular polymer (mmol) (mmol) (ml.) (mmol) (mmol) (g.) ...welght. (s-

(B)-I reparation of Cross-linked Copolymer The copolymer thus obatined was reacted with cyclopentadienylsodium at temperatures of 0 to 5" C. for 3 hours in a similar manner as in Example 9(B).

drochloric acid, washed repeatedly and thoroughly dried under reduced pressure to obtain an epichlorohydrintetrahydrofuran copolymer of a molecular weight of 3,150 in a yield of 434 g. The infrared absorption spectrum on the copolymer is shown in FIG. 7.

hours to conduct polymerization. The polymerizate was (B) Preparation of a Copolymer Having Pendant Cyclopentadiene Rings The copolymer obtained in said (A) was subjected to extraction with dried tetrahydrofuran by means of a 802(- lay extractor to prepare a polymer solution having a concentration of 3.0%. To the solution was then added dropwise at temperatures of to C. a tetrahydrofuran solution of cyclopentadienylsodium and the mixture was maintained at room temperature for 3 hours to conduct reaction. After completion of the reaction, the reaction mixture was concentrated and poured into water to obtain a precipitate which was thoroughly washed with methanol and dried under reduced pressure. The reaction conditions and results are summarized in the following copolymer).

1 Calculated on the basis of the C and Cl contents of the reaction product determined by elementary analysis.

-(C) Preparation of Cross-linked Copoly-mer Three reaction products having cyclopentadiene ring contents of 7.3, 9.8 and NJ mol percent were separately pressed at temperatures of 145 to 150 C. under a pressure of 50 kgJcm. for 1 hour to form sheets. The sheets were subjected to tests for determination of physical properties, the results obtained being summarized in Table 6.

TABLE 0 Tensile modulus Sheet 0 clopentad one 100% 200% Tensile at Elon a- Young's content, mol break on modulus percent KgJcm. (kg/cm!) (percent) (kg/cm!) What is claimed is:

1. A solid thermoplastic plastic composition comprising linear polymeric chains cross-linked into a substantially network structure through dicyclopentadiene rings of the formula:

said dicyclopentadiene rings being cleavable upon heating to a temperature above about 150 C. and refusable upon cooling below such temperature to recreate said cross-linked network structure.

2. A process for producing the thermoplastic plastic composition as in claim 1, which comprises dimerizing by heating up to about 150 C. a cyclopentadiene compound having one ethylenically unsaturated group to form a dicyclopentadiene compound having two ethylenically unsaturated groups and polymerizing the dicyclopentadiene compound either alone or in admixture with at least one other copolymerizable monomer.

3. A process for shaping the thermoplastic plastic composition as in claim 1, which comprise-s heating the plastic composition to a temperature above about-150? C. and sufficient to effect cleavage of the dicyclopentadiene rings to disrupt temporarily the cross-linked structure, manipulating the heated composition into the desired configuration, and then'cooling the composition below said temperature to recreate the cross-linked structure;

4. The normally solid thermoplastic addition homopolymer of a dicyclopentadiene monomer having two ethylenically unsaturated or glycidyl groups capable of undergoing addition polymerization. l

5. A solid thermoplastic plastic composition consisting of at least two linear polymeric chains, each such chain containing recurring lower alkylene groups and having only carbon and ether oxygen atoms linked therein, pairs of said chains being cross-linked together at recurrent intervals into a substantially network structure by dicyclopentadiene groups of the structure References Cited-- UNITED STATES PATENTS 3,277,036 10/1966 Whitworth et a1 260-23 3,414,548 12/1968- Bartl et aL 260-855 3,299,184 1/1967 Whitworth et al 260-897 2,985,635 '5/1961' Wasserman 26089.1 3,140,279 7/1964 :Spooncer 260-867 3,459,699 8/ 1969 JOSEPH L'. SHOFER, Primary Examiner J. KIGHT III, Assistant Examiner us. 01. xx.

260-78.4 E, EP, P, 82.1, 85.3, 86.7, 87.3, 88.1, R, PC, 88.2, B, D, E, 89.3, 91.1 R, A s, 93.1, 94.2, R, M, 94.7, R,A

Levine et al. 26029.7 

